Process for producing stabilized molten carbonate fuel cell porous anodes

Claim 2

A process for treatment of molten carbonate fuel cell porous metallic anodes to produce stabilized molten carbonate fuel cell porous metallic anodes comprising the steps of: impregnating a porous metallic anode comprising principally metal particles selected from the group consisting of: copper, cobalt, nickel and alloys and mixtures thereof, in an aqueous solution having dissolved therein a water soluble salt of a structure stabilizing agent; drying said impregnated porous anode at temperatures of about 80° C. to about 100° C. evaporating free water to form hydrated salts of said stabilizing agent on the surface of said metal particles; heating said impregnated dried porous anodes to a temperature of about 110° C. to about 160° C., dehydrating said hydrated compounds on the surface of said metal particles; and heating said porous anodes to a temperature of about 600° C. to about 700° C. in a reducing atmosphere forming particles of said stabilizing agent in reduced form on the surface of said metal particles.

Claim 3

The process of claim 1 wherein said water soluble salt is selected from the group consisting of chromium, zirconium, aluminum, and mixtures thereof.

Claim 4

The process of claim 1 wherein said water soluble salt is selected from the group consisting of lithium chromate, lithium dichromate, and mixtures thereof.

Claim 5

The process of claim 1 wherein said aqueous solution is a saturated solution of said water soluble salt.

Claim 6

The process of claim 1 wherein said metallic anode is impregnated by soaking in said aqueous solution for about 1 to about 15 minutes.

Claim 7

The process of claim 5 wherein a vacuum is applied to aid said impregnating.

Claim 8

The process of claim 1 wherein said drying is at about 85° to about 95° C.

Claim 9

The process of claim 1 wherein said dehydrating is at about 120° to about 140° C.

Claim 10

The process of claim 1 wherein said anodes are heated to a temperature of about 625° to about 675° C.

Claim 11

The process of claim 1 wherein said heating to about 600° to about 700° C. takes place in situ in a molten carbonate fuel cell.

Claim 12

The process of claim 10 wherein said water soluble salts comprise other than lithium salts and electrolyte of said molten carbonate fuel cell comprises at least one lithium compound.

Claim 13

The process of claim 1 wherein said stabilizing agent comprises about 0.5 to about 20 weight percent, based upon total anode weight.

Claim 14

The process of claim 1 wherein said stabilizing agent comprises about 1.0 to about 10 weight percent, based upon total anode weight.

Claim 15

The process of claim 1 wherein said water soluble salt is selected from the group consisting of chromium, zirconium, aluminum, and mixtures thereof, said aqueous solution is a saturated solution of said water soluble salt, and said stabilizing agent comprises about 0.5 to about 20 weight percent, based upon total anode weight.

Claim 16

The process of claim 14 wherein said heat treating to about 600° to about 700° C. takes place in a hydrogen-rich environment prior to assembly of said anode in said fuel cell.

Claim 17

The process of claim 1 wherein said water soluble salt is selected from the group consisting of chromium, zirconium, aluminum, and mixtures thereof, said aqueous solution is a saturated solution of said water soluble salt, said heating to about 600° to about 700° C. takes place in situ in a molten carbonate fuel cell, and said water soluble salts comprise other than lithium salts and electrolyte of said molten carbonate fuel cell comprises at least one lithium compound.

Claim 18

A process for producing stabilized molten carbonate fuel cell porous metallic anodes comprising the steps of: impregnating a porous metallic anode comprising principally metal particles selected from the group consisting of: copper, cobalt, nickel and alloys and mixtures thereof, in an aqueous solution having dissolved therein a water soluble salt of a structure stabilizing agent, said water soluble salt is selected from the group consisting of lithium chromate, lithium dichromate, potassium chromate, potassium dichromate, sodium chromate, sodium dichromate, chromic formate, chromous acetate, chromous formate, chromous oxalate, aluminum nitrate, zirconium nitrate, potassium aluminum oxide, and mixtures thereof; drying said impregnated porous anode at temperatures of about 80° C. to about 100° C. evaporating free water to form hydrated salts of said stabilizing agent on the surface of said metal particles; heating said impregnated dried porous anode to a temperature of about 110° C. to about 160° C., dehydrating said hydrated compounds on the surface of said metal particles; and heating said porous anode to a temperature of about 600° C. to about 700° C. in a reducing atmosphere forming particles of said stabilizing agent on the surface of said metal particles.

Claim 19

A process for producing stabilized molten carbonate fuel cell porous metallic anodes comprising the steps of: impregnating a porous metallic anode comprising principally metal particles selected from the group consisting of: copper, cobalt, nickel and alloys and mixtures thereof, in an aqueous solution having dissolved therein a water soluble salt of a structure stabilizing agent, said water soluble salt is selected from the group consisting of lithium chromate, lithium dichromate, potassium chromate, potassium dichromate, sodium chromate, sodium dichromate, chromic formate, chromous acetate, chromous formate, chromous oxalate, aluminum nitrate, zirconium nitrate, potassium aluminum oxide, and mixtures thereof; drying said impregnated porous anode at temperatures of about 80° C. to about 100° C. evaporating free water to form hydrated salts of said stabilizing agent on the surface of said metal particles; heating said impregnated dried porous anode to a temperature of about 110° C. to about 160° C., dehydrating said hydrated compounds on the surface of said metal particles; and heating said porous anode to a temperature of about 600° C. to about 700° C. in a reducing atmosphere forming particles of said stabilizing agent on the surface of said metal particles.

Claim 20

A process for producing stabilized molten carbonate fuel cell porous metallic anodes comprising the steps of: impregnating a porous metallic anode comprising principally metal particles selected from the group consisting of: copper, cobalt, nickel and alloys and mixtures thereof, in an aqueous solution having dissolved therein a water soluble salt of a structure stabilizing agent; drying said impregnated porous anode at temperatures of about 80° C. to about 100° C. evaporating free water to form hydrated salts of said stabilizing agent on the surface of said metal particles and repeating said impregnating and drying steps; heating said impregnated dried porous anode to a temperature of about 100° C. to about 160° C., dehydrating said hydrated compounds on the surface of said metal particles; and heating said porous anode to a temperature of about 600° C. to about 700° C. in a reducing atmosphere forming particles of said stabilizing agent on the surface of said metal particles.

Claim 21

A process for producing stabilized molten carbonate fuel cell porous metallic anodes comprising the steps of: impregnating a porous metallic anode comprising principally metal particles selected from the group consisting of: copper, cobalt, nickel and alloys and mixtures thereof, in an aqueous solution having dissolved therein a water soluble salt of a structure stabilizing agent; drying said impregnated porous anode at temperatures of about 80° C. to about 100° C. evaporating free water to form hydrated salts of said stabilizing agent on the surface of said metal particles and repeating said impregnating and drying steps; heating said impregnated dried porous anode to a temperature of about 100° C. to about 160° C., dehydrating said hydrated compounds on the surface of said metal particles; and heating said porous anode to a temperature of about 600° C. to about 700° C. in a reducing atmosphere forming particles of said stabilizing agent on the surface of said metal particles.

Claim 22

A process for producing stabilized molten carbonate fuel cell porous metallic anodes comprising the steps of: impregnating a porous metallic anode comprising principally metal particles selected from the group consisting of: copper, cobalt, nickel and alloys and mixtures thereof, in an aqueous solution having dissolved therein a water soluble salt of a structure stabilizing agent; drying said impregnated porous anode at temperatures of about 80° C. to about 100° C. evaporating free water to form hydrated salts of said stabilizing agent on the surface of said metal particles; heating said impregnated dried porous anode to a temperature of about 110° C. to about 160° C., dehydrating said hydrated compounds on the surface of said metal particles; and heating said porous anode to a temperature of about 600° C. to about 700° C. in a hydrogen-rich environment prior to assembly of said anode in said fuel cell forming particles of said stabillizing agent on the surface of said metal particles.

Claim 23

A process for producing stabilized molten carbonate fuel cell porous metallic anodes comprising the steps of: impregnating a porous metallic anode comprising principally metal particles selected from the group consisting of: copper, cobalt, nickel and alloys and mixtures thereof, in an aqueous solution having dissolved therein a water soluble salt of a structure stabilizing agent; drying said impregnated porous anode at temperatures of about 80° C. to about 100° C. evaporating free water to form hydrated salts of said stabilizing agent on the surface of said metal particles; heating said impregnated dried porous anode to a temperature of about 110° C. to about 160° C., dehydrating said hydrated compounds on the surface of said metal particles; and heating said porous anode to a temperature of about 600° C. to about 700° C. in a hydrogen-rich environment prior to assembly of said anode in said fuel cell forming particles of said stabillizing agent on the surface of said metal particles.

Claim 24

The process of claim 17 wherein said water soluble salt is selected from the group consisting of lithium chromate, lithium dichromate, and mixtures thereof.

Claim 25

The process of claim 17 wherein said aqueous solution is a saturated solution of said water soluble salt.

Claim 26

The process of claim 17 wherein said metallic anode is impregnated by soaking in said aqueous solution for about 1 to about 15 minutes.

Claim 27

The process of claim 17 wherein said drying is at about 85° to about 95° C.

Claim 28

The process of claim 17 wherein said dehydrating is at about 120° to about 140° C.

Claim 29

The process of claim 17 wherein said anodes are heated to a temperature of about 625° to about 675° C.

Claim 30

The process of claim 17 wherein said heating to about 600° to about 700° C. takes place in situ in a molten carbonate fuel cell.

Claim 31

The process of claim 26 wherein said water soluble salts comprise other than lithium salts and electrolyte of said molten carbonate fuel cell comprises at least one lithium compound.

Claim 32

The process of claim 17 wherein said stabilizing agent comprises about 0.5 to about 20 weight percent, based upon total anode weight.

Claim 33

The process of claim 17 wherein said stabilizing agent comprises about 1.0 to about 10 weight percent, based upon total anode weight.

Claim 34

The process of claim 17 wherein said water soluble salt is selected from the group consisting of chromium, zirconium, aluminum, and mixtures thereof, said aqueous solution is a saturated solution of said water soluble salt, and said stabilizing agent comprises about 0.5 to about 20 weight percent, based upon total anode weight.

Claim 35

The process of claim 17 wherein said water soluble salt is selected from the group consisting of chromium, zirconium, aluminum, and mixtures thereof, said aqueous solution is a saturated solution of said water soluble salt, said heating to about 600° to about 700° C. takes place in situ in a molten carbonate fuel cell, and said water soluble salts comprise other than lithium salts and electrolyte of said molten carbonate fuel cell comprises at least one lithium compound.